JPH03111435A - Styrene resin foam excellent in post expansion properties - Google Patents
Styrene resin foam excellent in post expansion propertiesInfo
- Publication number
- JPH03111435A JPH03111435A JP24923589A JP24923589A JPH03111435A JP H03111435 A JPH03111435 A JP H03111435A JP 24923589 A JP24923589 A JP 24923589A JP 24923589 A JP24923589 A JP 24923589A JP H03111435 A JPH03111435 A JP H03111435A
- Authority
- JP
- Japan
- Prior art keywords
- styrene resin
- resin foam
- foam
- styrene
- post expansion
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
Landscapes
- Manufacture Of Porous Articles, And Recovery And Treatment Of Waste Products (AREA)
- Blow-Moulding Or Thermoforming Of Plastics Or The Like (AREA)
Abstract
Description
【発明の詳細な説明】
(産業上の利用分野)
本発明は、加熱二次発泡成形性に優れ、発泡成形品の強
度に優れたスチレン系樹脂発泡体に関するものである。DETAILED DESCRIPTION OF THE INVENTION (Industrial Application Field) The present invention relates to a styrenic resin foam that has excellent heat secondary foaming moldability and excellent strength of the foam molded product.
(従来の技術および課題)
スチレン系樹脂発泡体は、加熱により二次発泡し、容易
に所望の形状に成形でき、かつ得られた成形体は軽量で
、機械的強度に優れ、外観が美しく、疎水性に富み、断
熱に優れているために、箱、トレー、カップ等の食品包
装材や簡易容器に使用されている。(Prior art and problems) Styrenic resin foam can be secondary-foamed by heating and easily molded into a desired shape, and the resulting molded product is lightweight, has excellent mechanical strength, and has a beautiful appearance. Because it is highly hydrophobic and has excellent heat insulation, it is used in food packaging materials such as boxes, trays, and cups, as well as simple containers.
最近、生産性の向上、不良率の減少の観点から、二次発
泡成形性の良好なスチレン系樹脂発泡体が望まれている
。Recently, styrenic resin foams with good secondary foaming moldability have been desired from the viewpoint of improving productivity and reducing defective rates.
シート状のスチレン系樹脂発泡体を加熱炉で加熱処理し
て発泡させ、次いで加熱炉から取り出して金型で成形す
る、一連の加熱二次発泡成形体の製造において、加熱炉
内の温度が不均一であることや、外気温による炉内温度
の変動のために、シートの一部、又は全部が加熱不足と
なり、成形時にシートが破れたり、成形品表面の一部が
かさぶた状になったり、型決まり性が悪くなったり、逆
に加熱過剰となって、成形品表面にケロイド状が発生し
たり、成形品の厚さが変動する等の減少が生じる。In the production of a series of heated secondary foamed products, in which sheet-shaped styrene resin foam is heat-treated in a heating furnace to foam, then taken out of the heating furnace and molded in a mold, the temperature inside the heating furnace is constant. Due to uniformity and fluctuations in the temperature inside the furnace due to outside air temperature, some or all of the sheet may be underheated, causing the sheet to tear during molding, or part of the surface of the molded product to form a crust. The moldability may deteriorate, or conversely, heating may become excessive, resulting in formation of keloids on the surface of the molded product, or variations in the thickness of the molded product.
ケロイド状の発生を防ぐために、基材のポリスチレン系
重合体の分子量を上げたり、シート表面にフィルムを貼
ったり、樹脂密度の大きい層、いわゆるスキン層を形成
したりする等の方法が知られているが、かかる方法では
型決まりの良い発泡体が得られにくく、とくに深絞り成
形品の場合には、シート破れが生じやすい。In order to prevent the formation of keloids, there are known methods such as increasing the molecular weight of the base polystyrene polymer, applying a film to the sheet surface, and forming a layer with high resin density, the so-called skin layer. However, with this method, it is difficult to obtain a foam with a well-defined shape, and sheet tearing is likely to occur, especially in the case of a deep-drawn product.
また、型決まり性の良い発泡体を得るために、ポリスチ
レン系重合体基材の分子量を下げたり、ポリスチレン系
重合体基材に可塑剤、滑、剤等を添加する方法が知られ
ているが、二次成形時の加熱過剰時に発生するケロイド
状の不良現象が起こりやすい。In addition, in order to obtain a foam with good shapeability, methods are known in which the molecular weight of the polystyrene polymer base material is lowered or plasticizers, lubricants, etc. are added to the polystyrene polymer base material. , keloid-like defects that occur during overheating during secondary molding are likely to occur.
ケロイド状の発生を抑え、型決まり性の良好なスチレン
系樹脂発泡体を得る方法として、分子量分布の広いスチ
レン系樹脂発泡体を使用することが有効であることが、
特開昭62−22834号公報に記載されている。しか
し、かかる分子量分布の広いスチレン系樹脂発泡体の成
形品は本質的に強度が弱いという欠点を有している。The use of a styrene resin foam with a wide molecular weight distribution is effective as a method for suppressing the occurrence of keloids and obtaining a styrenic resin foam with good moldability.
It is described in Japanese Patent Application Laid-Open No. 62-22834. However, such molded products made of styrene resin foams having a wide molecular weight distribution inherently have a drawback of low strength.
(課題を解決するための手段)
本発明者らは、かかる現状に鑑み、スチレン系重合体中
に長鎖のアルキル鎖を導入することにより、二次加熱成
形時、ケロイド状の発生を抑え、型決まり性が良好であ
り、深絞り性に優れたスチレン系樹脂発泡体を開発すべ
く鋭意検討した結果1、本発明を完成するに至った。(Means for Solving the Problems) In view of the current situation, the present inventors introduced a long alkyl chain into a styrene polymer to suppress the formation of keloids during secondary heat molding. As a result of intensive studies to develop a styrenic resin foam that has good shaping properties and excellent deep drawability, the present invention has been completed.
すなわち、本発明は;
■ 重量平均分子量が15万〜50万であって、120
°Cで測定した応力緩和の初期緩和弾性率と150″C
で測定した応力緩和の初期緩和弾性率の比が1〜2.5
の範囲にある二次成形性に優れたスチレン系樹脂発泡体
を提供するものである。That is, the present invention has; (i) a weight average molecular weight of 150,000 to 500,000, and 120
Initial relaxation modulus of stress relaxation measured at °C and 150″C
The ratio of the initial relaxation modulus of stress relaxation measured at is 1 to 2.5.
The object of the present invention is to provide a styrenic resin foam having excellent secondary moldability within the range of .
また、■ スチレン系樹脂発泡体の厚さが0゜5〜5■
、嵩密度0.03〜0.3 g/cm3のシート状であ
る、二次成形性に優れたスチレン系樹脂発泡体でもある
。In addition, ■ The thickness of the styrene resin foam is 0°5~5■
It is also a styrenic resin foam with excellent secondary moldability, which is in the form of a sheet with a bulk density of 0.03 to 0.3 g/cm3.
以下、本発明をさらに詳しく説明する。The present invention will be explained in more detail below.
スチレン系樹脂発泡体の重量平均分子量は15万〜50
万、より好ましくは20万〜45万である0重量平均分
子量が15万未満では発泡成形品の強度が弱く、実用に
耐ええない、また、重量平均分子量が50万を越える場
合には、二次発泡成形時の型決まり性が著しく悪くなる
。The weight average molecular weight of styrene resin foam is 150,000 to 50
If the weight average molecular weight is less than 150,000, the strength of the foamed molded product will be weak and cannot be used in practical use. The moldability during the subsequent foam molding becomes significantly worse.
なお、本発明では、発泡体基材であるスチレン系重合体
の分子量はGPC測定法により、東洋曹達工業■製GP
C(HLC−802A) 、同社製GPC用カラム(T
SK−C,EL−C;MHを二本使用)を用いて測定し
た。In addition, in the present invention, the molecular weight of the styrene polymer that is the foam base material is determined by GPC measurement method using GP manufactured by Toyo Soda Kogyo.
C (HLC-802A), the same company's GPC column (T
SK-C, EL-C; two MHs were used).
本発明のスチレン系樹脂発泡体は、l 20 ℃で測定
した応力緩和の初期緩和弾性率と150 ℃で測定した
応力緩和の初1tlltil和弾性率の比が、1〜2.
5の範囲にあることが必要であり、より好ましくは1.
2〜2.3の範囲である。The styrenic resin foam of the present invention has a ratio of the initial relaxation modulus of stress relaxation measured at 120°C to the initial 1 tlltil sum elastic modulus of stress relaxation measured at 150°C of 1 to 2.
5, more preferably 1.
It is in the range of 2 to 2.3.
この120°C/150°Cの比が1より小さいと二次
発泡成形品の型決まり性が悪く、2.5を越えると二次
発泡成形時の深絞り性が悪くなる。If the ratio of 120°C/150°C is less than 1, the moldability of the secondary foamed product will be poor, and if it exceeds 2.5, the deep drawability during secondary foaming will be poor.
なお、応力緩和の初期緩和弾性率は、勝山ら著、王化誌
71S4号540〜545頁(1968年)に述べられ
ている方法に従って測定する。Note that the initial relaxation modulus of stress relaxation is measured according to the method described in Katsuyama et al., No. 71 S4, pages 540-545 (1968).
ここで、初!IJII和弾性率とは、歪みを与えた瞬間
に得られる緩和弾性率を言う。供するサンプルは、発泡
体の場合にはあらかじめ気泡を抜いた固形状にしておく
。発泡前のペレットを利用しても良い。First time here! The IJII sum modulus refers to the relaxation modulus obtained at the moment of applying strain. If the sample to be used is a foam, the air bubbles should be removed beforehand to make it solid. Pellets before foaming may be used.
120″Cで測定した応力緩和の初期緩和弾性率と15
0 ℃で測定した応力緩和の初期緩和弾性率の比が、1
〜2.5の範囲にあるようなスチレン系樹脂は、例えば
次のようにして調製することができるが、これに限定さ
れるわけではない。Initial relaxation modulus of stress relaxation measured at 120″C and 15
The ratio of the initial relaxation modulus of stress relaxation measured at 0 °C is 1
A styrenic resin having a molecular weight in the range of 2.5 to 2.5 can be prepared, for example, as follows, but is not limited thereto.
−数式(■):
(式中、l、m、nは1〜20の整数であり、R+ 、
Rz 、R3、R−は水素、炭素数1〜5のアルキル基
、シクロヘキシル基、あるいはフェニル基である。)
で示される繰り返し単位3個以上、好ましくは5〜30
個を有する低温分解性有機過酸化物開始剤を用いて、ス
チレン系単量体を重合する。- Formula (■): (In the formula, l, m, and n are integers from 1 to 20, and R+,
Rz, R3, and R- are hydrogen, an alkyl group having 1 to 5 carbon atoms, a cyclohexyl group, or a phenyl group. ) 3 or more repeating units, preferably 5 to 30 repeating units
A styrenic monomer is polymerized using a low-temperature decomposable organic peroxide initiator having
このような開始剤として、例えば次のような繰り返し単
位を有するものが使用できる。As such an initiator, for example, those having the following repeating units can be used.
このような重合法の採用により、長鎖アルキル基が導入
されたスチレン系重合体が生成する。By employing such a polymerization method, a styrenic polymer into which a long-chain alkyl group is introduced is produced.
この場合に、重合時に、(開始剤の10時間半減期温度
)〜(開始剤の10時間半減期温度+70°C)の範囲
の温度で、重合率が少なくとも10重量%以上になるま
で予備重合を行い、その後、任意の温度で重合を進める
ことにより、スチレン系重合体中に長鎖のアルキル鎖を
好適に導入できる。In this case, during polymerization, prepolymerization is carried out at a temperature in the range of (initiator's 10-hour half-life temperature) to (initiator's 10-hour half-life temperature + 70°C) until the polymerization rate reaches at least 10% by weight. By carrying out the above steps and then proceeding with the polymerization at an arbitrary temperature, a long alkyl chain can be suitably introduced into the styrenic polymer.
本発明のスチレン系重合体は、前述の方法で長鎖のアル
キル鎖を導入できるが、重合方法は特に限定されるもの
ではない。塊状重合、溶液重合、懸濁重合等公知の方法
を用いることができる。また、公知の有機過酸化物と併
用してもよく、あるいは、途中添加してもよい、また、
溶媒などを用いることもできる。Although long alkyl chains can be introduced into the styrenic polymer of the present invention by the method described above, the polymerization method is not particularly limited. Known methods such as bulk polymerization, solution polymerization, and suspension polymerization can be used. In addition, it may be used in combination with a known organic peroxide, or it may be added during the process.
A solvent or the like can also be used.
使用されるスチレン系単量体としては、スチレン、α−
メチルスチレン、ビニルトルエン、p−メチルスチレン
などの単独あるいはそれらを組合せて使用できる。また
、本発明のスチレン系単量体と共に、必要に応じてアク
リル酸、メタクリル酸、アクリル酸メチル、メタクリル
酸メチル、無水マレイン酸等のビニル系単量体を混合使
用してもよい。Styrene monomers used include styrene, α-
Methylstyrene, vinyltoluene, p-methylstyrene, etc. can be used alone or in combination. In addition, a vinyl monomer such as acrylic acid, methacrylic acid, methyl acrylate, methyl methacrylate, or maleic anhydride may be used in combination with the styrene monomer of the present invention, if necessary.
とくに、重合条件は、分子量を調整する他、オリゴマー
(スチレン系二量体、二量体などのビニル系オリゴマー
)含有量ができるだけ少な(なるようにすることが望ま
しい、オリゴマー含有量は好ましくは、0.5重量%以
下である。In particular, the polymerization conditions should be adjusted so that the molecular weight is adjusted, and the oligomer content (vinyl oligomers such as styrene dimers and dimers) is as low as possible. It is 0.5% by weight or less.
オリゴマー含有量は、ガスクロマトグラフィーや液体ク
ロマトグラフィーで測定できる。さらに、必要に応じて
、滑剤や、ミネラルオイルなどの可塑剤、酸化防止剤な
どが含まれてもよい。Oligomer content can be measured by gas chromatography or liquid chromatography. Furthermore, if necessary, a lubricant, a plasticizer such as mineral oil, an antioxidant, etc. may be included.
長鎖のアルキル鎖をもつスチレン系樹脂の定量は、以下
のようにして行った。The styrenic resin having a long alkyl chain was quantified as follows.
スチレン系重合体発泡体を10倍量のメチルエチルケト
ンに溶解後、同量のメタノールをゆっくり添加しながら
、スチレン系重合体を析出させる。After dissolving the styrenic polymer foam in 10 times the amount of methyl ethyl ketone, the same amount of methanol is slowly added to precipitate the styrenic polymer.
析出したスチレン系重合体を200°C15s Hgの
減圧下で30分乾燥する。このスチレン系重合体を用い
て、日本電子■のJNM−GX270を用いて13Cを
測定する。以下の測定条件で測定した。The precipitated styrenic polymer is dried at 200° C. under reduced pressure of 15 s Hg for 30 minutes. Using this styrene polymer, 13C is measured using JNM-GX270 manufactured by JEOL Ltd. Measurement was performed under the following measurement conditions.
完全デカップリングモード−45°パルス、観測周波数
=67.8MH2、
待ち時間−2,5秒、
スキャン回数=ioo、ooo回、
サンプル濃度=l Qwt%、
溶媒=1.1−テトラクロロエタン(d2)、サンプル
管−10閣、
測定温度=120°C0
長鎖のアルキル鎖のメチレン基の炭素に由来するピーク
が29.4ppmに現れる。また、長鎖中の第4級炭素
に隣接する炭素に由来するピークが33.7ppmに現
れる。このピークの存在を確認することにより、スチレ
ン系重合体中に構成単位(1)の存在の有無を確認でき
る。Complete decoupling mode - 45° pulse, observation frequency = 67.8MH2, waiting time - 2.5 seconds, number of scans = ioo, ooo times, sample concentration = l Qwt%, solvent = 1.1-tetrachloroethane (d2) , Sample tube-10, Measurement temperature = 120° C0 A peak derived from the carbon of the methylene group of the long alkyl chain appears at 29.4 ppm. Furthermore, a peak derived from the carbon adjacent to the quaternary carbon in the long chain appears at 33.7 ppm. By confirming the presence of this peak, it is possible to confirm the presence or absence of the structural unit (1) in the styrenic polymer.
他の測定方法として、島原製作所のDSC−41を用い
て、DSC分析を行い、発泡体基材であるスチレン系重
合体のTgより求めることも可能である。”C−NMR
測定と同様に処理されたサンプルを用いて、8°C/分
の昇温速度で測定する。As another measurement method, it is also possible to perform DSC analysis using DSC-41 manufactured by Shimabara Seisakusho and determine the Tg of the styrene polymer that is the foam base material. “C-NMR
The measurement is carried out using a sample treated in the same manner as in the measurement, at a heating rate of 8°C/min.
スチレン系樹脂発泡体は、スチレン系樹脂にプロパン、
ブタン、ペンタン、ヘキサン等の低級炭化水素や塩化メ
チル、ジクロロメタン、トリクロロモノフルオロメタン
、ジクロロジフルオロメタン等のハロゲン化炭化水素等
の発泡剤を含浸させて、押出機に供給するか、スチレン
系樹脂を押出機に供給した後、押出機中に上記発泡剤を
圧入し、発泡剤とスチレン系樹脂を押出機で溶融・混練
させ、Tダイ又はサーキュラ−ダイなどから押し出すな
どの公知の方法により、厚さが0.5〜5IIIli1
嵩密度が0.03〜0.3g/c−のシート状の一次発
泡されたポリスチレン系発泡体が製造される。Styrenic resin foam uses styrene resin and propane.
Either blowing agents such as lower hydrocarbons such as butane, pentane, and hexane or halogenated hydrocarbons such as methyl chloride, dichloromethane, trichloromonofluoromethane, and dichlorodifluoromethane are impregnated and fed to an extruder, or styrene resin is After supplying the foaming agent to the extruder, the foaming agent is press-fitted into the extruder, the foaming agent and styrene resin are melted and kneaded in the extruder, and the thickness is increased by a known method such as extruding from a T-die or circular die. Saga 0.5-5IIIli1
A sheet-like primary foamed polystyrene foam having a bulk density of 0.03 to 0.3 g/c is produced.
−次発泡されたシートの厚さは、0.5〜5鮒が好まし
い、厚さが0.58よりも薄いと二次発泡時にシートが
破損したり、十分な成形品強度を有しない。また、厚さ
が5閣を越えると二次成形が困難になる。- The thickness of the post-foamed sheet is preferably 0.5 to 5 mm. If the thickness is thinner than 0.58, the sheet may be damaged during the post-foaming or the molded product will not have sufficient strength. Further, if the thickness exceeds five layers, secondary forming becomes difficult.
嵩密度は0.03〜0.3g/dが好ましい。The bulk density is preferably 0.03 to 0.3 g/d.
嵩密度が0.03g/dより小さいと二次発泡時にシー
トが破れたり、成形品強度が十分でなく、0.3g/c
jより大きいと発泡品としてのメリットが減じる。If the bulk density is less than 0.03 g/d, the sheet may be torn during secondary foaming or the strength of the molded product may not be sufficient;
If it is larger than j, the merits as a foamed product will be reduced.
スチレン系樹脂を発泡させ、スチレン系樹脂発泡体を得
るに当たり、発泡セル径を制御するタルク、炭酸カルシ
ウム等の造核剤、可塑剤、滑剤、顔料、帯電防止剤、酸
化防止剤、難燃剤などを混合使用してもよい。また、得
られたスチレン系樹脂発泡体の表面特性を変えるために
、帯電防止剤、シリコーンなどの滑剤を表面に塗布して
もよい。When foaming styrene resin to obtain styrene resin foam, nucleating agents such as talc and calcium carbonate to control the foam cell diameter, plasticizers, lubricants, pigments, antistatic agents, antioxidants, flame retardants, etc. may be used in combination. Furthermore, in order to change the surface properties of the obtained styrenic resin foam, an antistatic agent, a lubricant such as silicone, etc. may be applied to the surface.
本発明で意図する発泡体の機能を損なわない範囲で、前
記長鎖アルキル鎖を導入した特定のスチレン系重合体に
他のスチレン系重合体を混合して使用することも可能で
ある。It is also possible to mix and use other styrenic polymers with the specific styrenic polymer into which the long alkyl chains have been introduced, as long as the functionality of the foam intended in the present invention is not impaired.
以上のようにして得られたスチレン系樹脂発泡体を加熱
二次発泡成形するには、スチレン系樹脂発泡体を加熱炉
にいれて、軟化、二次発泡させた後、加熱炉から出し、
直ちにプレス金型でプレス成形して成形品にするのが一
般的である。In order to heat and secondary foam the styrene resin foam obtained as described above, the styrenic resin foam is placed in a heating furnace, softened and secondary foamed, and then taken out of the heating furnace.
Generally, the product is immediately press-molded using a press mold to form a molded product.
本発明のスチレン系樹脂発泡体は、広い加熱温度幅に於
いて均一な軟化状態が得られる為、加熱炉の温度変化、
加熱炉内に温度分布等によるケロイド状が発生しにくく
、型決まり性の良好な成形品が得られ特に探しぼり性の
優れた成形品が得られる。The styrenic resin foam of the present invention can obtain a uniform softening state over a wide heating temperature range, so
Keloid-like formations due to temperature distribution etc. in the heating furnace are less likely to occur, and molded products with good shaping properties can be obtained, and in particular, molded products with excellent findability can be obtained.
以下、実施例に基づき本発明を具体的に説明するが、こ
れらは本発明の範囲を制限するものでない。EXAMPLES Hereinafter, the present invention will be specifically explained based on Examples, but these are not intended to limit the scope of the present invention.
実施例1
スチレン単f体90重世%、エチルベンゼン10重量%
の混合液100重量部に対し、下記の繰返し単位を有す
る開始剤を0.5重量部添加して、110℃で6時間、
145°Cで5時間重合し、未反応スチレン単量体及び
エチルベンゼンなどは230°Cl3mmHgで脱揮し
て、ポリスチレンを得た。その分析値を表1に示す。Example 1 Styrene single F 90% by weight, ethylbenzene 10% by weight
To 100 parts by weight of the mixed solution, 0.5 parts by weight of an initiator having the following repeating unit was added, and the mixture was heated at 110°C for 6 hours.
Polymerization was carried out at 145°C for 5 hours, and unreacted styrene monomers, ethylbenzene, etc. were devolatilized at 230°C and 3 mmHg to obtain polystyrene. The analytical values are shown in Table 1.
このポリスチレンの初期緩和弾性率を、勝山ら、王化誌
、71巻、4号、540〜545頁(1968年)に述
べられている方法に従って測定し、150℃で5. O
X I O’dyn/c4.120℃で1゜OX l
O”dyn/ cdの値を得た。The initial relaxation modulus of this polystyrene was measured according to the method described in Katsuyama et al., Wangka Journal, Vol. 71, No. 4, pp. 540-545 (1968), and the initial relaxation modulus was measured at 150°C. O
X I O'dyn/c4.1゜OX l at 120℃
The value of O”dyn/cd was obtained.
このポリスチレンにタルクを0.25重量%をあらかじ
め混合し、50mmφの押出機に供給し、205°Cで
溶融させた。押出機の先端部分にフロン−12を5重量
%圧入し、第2の押出機に導いて150°Cまで冷却し
た。This polystyrene was mixed in advance with 0.25% by weight of talc, supplied to a 50 mmφ extruder, and melted at 205°C. 5% by weight of Freon-12 was press-fitted into the tip of the extruder, led to a second extruder, and cooled to 150°C.
次いで、サーキュラ−グイより筒形発泡シートを得、1
ケ所にて切開いて厚さ2.0mm、嵩密度0.12/c
−のスチレン系樹脂発泡体シートを得た。このスチレン
系樹脂発泡体を1ケ月間養生し、イリッヒ成形機に付属
している赤外線加熱炉で125℃に加熱し、二次発泡さ
せ、加熱時間を変えながら、深絞り部分のある成形品を
成形して、各シートの二次成形性を評価した。評価結果
を表1に示す。Next, a cylindrical foam sheet was obtained from a circular gui, and 1
Incisions were made at two locations to obtain a thickness of 2.0 mm and a bulk density of 0.12/c.
- A styrenic resin foam sheet was obtained. This styrene resin foam was cured for one month, then heated to 125°C in an infrared heating furnace attached to the Illich molding machine to cause secondary foaming, and while changing the heating time, molded products with deep drawing parts were formed. The sheets were molded and the secondary moldability of each sheet was evaluated. The evaluation results are shown in Table 1.
実施例2
スチレン単量体97重量%、エチルベンゼン3重量%の
混合液100重量部を用いた他は、実施例1と同様に実
験した。その結果を表1に示す。Example 2 An experiment was carried out in the same manner as in Example 1, except that 100 parts by weight of a mixed solution of 97% by weight of styrene monomer and 3% by weight of ethylbenzene was used. The results are shown in Table 1.
比較例1
スチレン単量体90重量%、エチルベンゼン10重量%
の混合液を、開始剤を用いずに120°Cで6時間、1
50°Cで5時間重合した他は、実施例1と同様に実験
した。その結果を表1に示す。Comparative Example 1 Styrene monomer 90% by weight, ethylbenzene 10% by weight
The mixture was incubated at 120°C for 6 hours without initiator for
The experiment was carried out in the same manner as in Example 1, except that the polymerization was carried out at 50°C for 5 hours. The results are shown in Table 1.
比較例2
;lチレ7単量体97ffiffi%、エチルベンゼン
3重量%の混合液100重量部に対し、L−プチルパー
ヘンゾエート0.3重量部を添加し、100°Cで6時
間140 ℃で5時間重合した他は、実施例1と同様に
実験した。その結果を表1に示す。Comparative Example 2; 0.3 parts by weight of L-butylperhenzoate was added to 100 parts by weight of a mixed solution of 97% of L-chile 7 monomer and 3% by weight of ethylbenzene, and the mixture was incubated at 100°C for 6 hours at 140°C. The experiment was carried out in the same manner as in Example 1, except that the polymerization was carried out for 5 hours. The results are shown in Table 1.
(発明の効果)
本発明のスチレン系樹脂発泡体は、二次成形時に少ない
加熱時間でも破断や表面のかさぶた状が発生せず、かつ
型決まり性が良好で、また加熱時間が長めになっても成
形品のへたりやケロイド状が発生しにくく、深絞りに広
い条件中で耐えられる効果がある。(Effects of the Invention) The styrenic resin foam of the present invention does not cause breakage or crusting on the surface even with a short heating time during secondary molding, has good moldability, and has a long heating time. Also, molded products are less prone to sagging or keloid formation, and can withstand deep drawing under a wide range of conditions.
(ほか1名)(1 other person)
Claims (2)
0℃で測定した応力緩和の初期緩和弾性率と150℃で
測定した応力緩和の初期緩和弾性率の比が1〜2.5の
範囲にあることを特徴とする、二次成形性に優れたスチ
レン系樹脂発泡体。(1) Weight average molecular weight is 150,000 to 500,000, and 12
Excellent secondary formability, characterized in that the ratio of the initial relaxation modulus of stress relaxation measured at 0°C and the initial relaxation modulus of stress relaxation measured at 150°C is in the range of 1 to 2.5. Styrenic resin foam.
嵩密度0.03〜0.3g/cm^3のシート状である
、請求項(1)記載のスチレン系樹脂発泡体。(2) The thickness of the styrene resin foam is 0.5 to 5 mm,
The styrenic resin foam according to claim 1, which is in the form of a sheet having a bulk density of 0.03 to 0.3 g/cm^3.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP24923589A JP2942791B2 (en) | 1989-09-27 | 1989-09-27 | Styrene resin foam with excellent secondary moldability |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP24923589A JP2942791B2 (en) | 1989-09-27 | 1989-09-27 | Styrene resin foam with excellent secondary moldability |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH03111435A true JPH03111435A (en) | 1991-05-13 |
| JP2942791B2 JP2942791B2 (en) | 1999-08-30 |
Family
ID=17189936
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP24923589A Expired - Lifetime JP2942791B2 (en) | 1989-09-27 | 1989-09-27 | Styrene resin foam with excellent secondary moldability |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP2942791B2 (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0987332A (en) * | 1995-09-28 | 1997-03-31 | Asahi Chem Ind Co Ltd | Styrene- (meth) acrylic acid-based copolymer and composition thereof |
-
1989
- 1989-09-27 JP JP24923589A patent/JP2942791B2/en not_active Expired - Lifetime
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0987332A (en) * | 1995-09-28 | 1997-03-31 | Asahi Chem Ind Co Ltd | Styrene- (meth) acrylic acid-based copolymer and composition thereof |
Also Published As
| Publication number | Publication date |
|---|---|
| JP2942791B2 (en) | 1999-08-30 |
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